JPH0221501B2 - - Google Patents
Info
- Publication number
- JPH0221501B2 JPH0221501B2 JP14428581A JP14428581A JPH0221501B2 JP H0221501 B2 JPH0221501 B2 JP H0221501B2 JP 14428581 A JP14428581 A JP 14428581A JP 14428581 A JP14428581 A JP 14428581A JP H0221501 B2 JPH0221501 B2 JP H0221501B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- absorption
- condenser
- liquid
- heat pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000010521 absorption reaction Methods 0.000 claims description 51
- 239000007788 liquid Substances 0.000 claims description 34
- 239000003507 refrigerant Substances 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000000498 cooling water Substances 0.000 claims description 14
- 239000012530 fluid Substances 0.000 claims description 7
- 239000006096 absorbing agent Substances 0.000 claims description 5
- 239000002699 waste material Substances 0.000 description 6
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000002159 abnormal effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は吸収液による冷媒吸収の温度が吸収液
から冷媒を発生させる温度よりも高く、かつ、冷
媒の蒸発温度が冷媒の凝縮温度よりも高く設定さ
れた吸収ヒートポンプ(以下単に吸収ヒートポン
プという)に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides an absorption heat pump ( (hereinafter simply referred to as an absorption heat pump).
一般に、冷凍機は冷却側と放熱側とを有し、冷
却側を利用するときはいわゆる冷凍機、放熱側を
利用するときはヒートポンプと称し、圧縮式、吸
収式を問わず殆どのヒートポンプがこのような概
念に入る。 In general, a refrigerator has a cooling side and a heat radiation side.When the cooling side is used, it is called a refrigerator, and when the heat radiation side is used, it is called a heat pump.Most heat pumps, regardless of compression type or absorption type, into such a concept.
しかし、本発明の吸収ヒートポンプは上記の概
念と異なつたヒートポンプ専用の吸収機であり、
低温度レベルの熱で冷媒を蒸発させ、冷媒蒸気を
吸収液に吸着させるときに発生する吸収熱により
高温の温水を取り出すようにしたヒートポンプ、
すなわち、冷媒の吸収温度が冷媒の発生温度より
も高く、また冷媒の蒸発温度がその凝縮温度より
も高いタイプの吸収ヒートポンプに関するもので
ある。 However, the absorption heat pump of the present invention is an absorption machine exclusively for heat pumps, which is different from the above concept.
A heat pump that uses low-temperature heat to evaporate refrigerant and extracts high-temperature hot water using the absorption heat generated when the refrigerant vapor is adsorbed by an absorption liquid.
That is, the present invention relates to an absorption heat pump of a type in which the refrigerant absorption temperature is higher than the refrigerant generation temperature, and the refrigerant evaporation temperature is higher than its condensation temperature.
図はこのような吸収ヒートポンプの一例を示
し、上胴1に蒸発器2及び吸収器3が、下胴4に
発生器5及び凝縮器6がそれぞれ収められ、これ
らの器体は冷媒ポンプ7を有する冷媒管8、吸収
液ポンプ9を有する吸収液管10、吸収液戻し管
11、熱交換器12などを介して気密に接続され
ており、蒸発器2には液冷媒溜13と液冷媒を蒸
発器2の上部から散布する冷媒循環ポンプ14が
配設され、発生器5と蒸発器2とにはそれぞれ廃
温水、廃蒸気など低温レベルの熱源流体(以下低
温熱源という)が供給されて吸収ヒートポンプ系
に熱を与える給熱熱交換器15,16が、凝縮器
6には発生器5で気化した冷媒を冷却し液化する
冷却器17が内蔵されており、吸収器3の温水熱
交換器18から給湯用或いは暖房用の温水が取り
出せるようにしている。 The figure shows an example of such an absorption heat pump, in which an evaporator 2 and an absorber 3 are housed in an upper body 1, a generator 5 and a condenser 6 are housed in a lower body 4, and a refrigerant pump 7 is housed in these bodies. The evaporator 2 has a liquid refrigerant reservoir 13 and a liquid refrigerant connected to the evaporator 2 through a refrigerant pipe 8 having a liquid refrigerant, an absorption liquid pipe 10 having an absorption liquid pump 9, an absorption liquid return pipe 11, a heat exchanger 12, etc. A refrigerant circulation pump 14 is disposed to spray from the upper part of the evaporator 2, and the generator 5 and the evaporator 2 are each supplied with low-temperature heat source fluids (hereinafter referred to as low-temperature heat sources) such as waste hot water and waste steam, and absorb them. The heat supply heat exchangers 15 and 16 provide heat to the heat pump system, the condenser 6 has a built-in cooler 17 that cools and liquefies the refrigerant vaporized by the generator 5, and the hot water heat exchanger of the absorber 3 Hot water for hot water supply or heating can be taken out from 18.
例えば、吸収液に臭化リチウム、冷媒に水を用
い低温熱源に約90℃の廃蒸気D冷却水に30℃前後
の水Cを用いたとき、第2図のデユーリング線図
に示すように略130℃に昇温された熱水Hが温水
熱交換器18から得られる。 For example, when using lithium bromide as the absorption liquid, water as the refrigerant, waste steam at about 90°C as the low-temperature heat source, and water C at around 30°C as the cooling water, the following diagram will appear as shown in the Duering diagram in Figure 2. Hot water H heated to 130°C is obtained from the hot water heat exchanger 18.
而して、斯る吸収ヒートポンプの吸収液は従来
の吸収式のヒートポンプより高い濃度で運転され
る状態があるため、ヒートポンプ運転を停止する
ときは確実に吸収液が稀釈されていることが必要
である。又、従来から吸収式のヒートポンプにお
いては、熱源流体の流量を制御して運転制御をす
るのが普通であるが、熱源に廃蒸気等の工場排熱
を利用するときは、熱源の制御が元の工場に幣害
を伴なうためにこのような制御方式をとれないこ
とがあり、又、吸収ヒートポンプを循環する吸収
液の濃度が他の条件によつて変化し、取り出し温
水温度が変動したり、吸収液の結晶を生じて吸収
ヒートポンプの運転が不能となるおそれがあつ
た。 Therefore, since the absorption liquid of such absorption heat pumps is operated at a higher concentration than that of conventional absorption heat pumps, it is necessary to ensure that the absorption liquid is diluted when stopping heat pump operation. be. In addition, in conventional absorption heat pumps, operation is normally controlled by controlling the flow rate of the heat source fluid, but when using factory waste heat such as waste steam as the heat source, control of the heat source is the primary method. In some cases, such a control method cannot be used because it would cause damage to the factory, and the concentration of the absorption liquid circulating in the absorption heat pump may change depending on other conditions, causing the temperature of the hot water taken out to fluctuate. Otherwise, there was a risk that the absorption liquid would crystallize, making it impossible to operate the absorption heat pump.
このような点に鑑みなされた本発明は、低温熱
源に廃蒸気や廃温水を使用し、冷却水に海水や工
業用水などを使用して高温度レベルの温水又は蒸
気を発生させる吸収ヒートポンプの安定した運転
を可能にしたものであり、該ヒートポンプの定常
運転時には凝縮器内の液温(又は圧力)を略一定
に保ち、かつ、運転停止時には凝縮器内の液温を
高めるような制御機構を付設するようにしたもの
である。 The present invention was created in view of these points, and is aimed at stabilizing an absorption heat pump that uses waste steam or waste hot water as a low-temperature heat source and uses seawater or industrial water as cooling water to generate high-temperature level hot water or steam. The heat pump has a control mechanism that keeps the liquid temperature (or pressure) in the condenser almost constant during steady operation, and increases the liquid temperature in the condenser when the operation is stopped. It was designed to be attached.
図において、19は凝縮器内の冷媒溜21の温
度センサ20、凝縮器6を冷却する冷却水の出口
温度のセンサ22又は凝縮器内の圧力のセンサ2
3等の中の一つ又はこれらの複合のデータを入力
信号とした制御器、24は該制御器19により、
冷却器17への水量を制御する制御弁であり、該
制御器19は凝縮器内の温度(又は圧力)或いは
冷却水の温度が低下しつつあるときは弁24を絞
り、これらのいずれかが設定値より上昇する傾向
にあるときは弁24を開放するように制御する機
構を有している。 In the figure, 19 is a temperature sensor 20 of the refrigerant reservoir 21 in the condenser, a sensor 22 of the outlet temperature of the cooling water that cools the condenser 6, or a sensor 2 of the pressure in the condenser.
A controller 24 which uses one of the above or a combination of these data as an input signal, is controlled by the controller 19.
This is a control valve that controls the amount of water to the cooler 17, and the controller 19 throttles the valve 24 when the temperature (or pressure) in the condenser or the temperature of the cooling water is decreasing, and when either of these is It has a mechanism that controls to open the valve 24 when the temperature tends to rise above the set value.
而して、此の種の吸収ヒートポンプにおいては
発生器5における吸収液からの冷媒発生量および
吸収器3に供給される吸収液の濃度が、発生器3
及び蒸発器2に供給される低温熱源を一定温度と
すると、略一義的に凝縮器6の冷却水温度で決ま
るため、冷却水(例えば、海水や地下水などの天
然水)の温度が季節によつて変動した場合に、制
御器19によつて、上述のように、制御弁24の
開度を調整すると、この吸収ヒートポンプから取
り出す温水温度を一定化し、吸収液の結晶を生じ
る幣害なく吸収ヒートポンプを安定に運転するこ
とができる。 In this type of absorption heat pump, the amount of refrigerant generated from the absorption liquid in the generator 5 and the concentration of the absorption liquid supplied to the absorber 3 are
If the temperature of the low-temperature heat source supplied to the evaporator 2 is constant, the temperature of the cooling water in the condenser 6 is almost uniquely determined, so the temperature of the cooling water (for example, natural water such as seawater or groundwater) varies depending on the season. When the temperature of the absorption heat fluctuates, when the opening degree of the control valve 24 is adjusted by the controller 19 as described above, the temperature of the hot water taken out from the absorption heat pump is kept constant, and the absorption heat pump can be operated stably.
すなわち、蒸発器2及び発生器5に低温熱源が
一定の温度で供給されているとき、制御弁24を
開いて冷却水量を増やすと、凝縮温度が低下し、
発生器5における吸収液からの冷媒発生量が増加
し、凝縮器6への冷媒分離量を増加させると共に
吸収液濃度を上昇させることができ、逆に、制御
弁24を絞れば、発生器5からの冷媒発生量を減
らし、吸収液濃度を低下させるなど、凝縮器6内
部の温度(圧力)の制御によつて、吸収液の濃度
を安定化し、取り出し温水温度を一定化できるも
のである。 That is, when the low-temperature heat source is supplied to the evaporator 2 and the generator 5 at a constant temperature, when the control valve 24 is opened to increase the amount of cooling water, the condensation temperature decreases,
The amount of refrigerant generated from the absorption liquid in the generator 5 increases, increasing the amount of refrigerant separated into the condenser 6 and increasing the concentration of the absorption liquid. By controlling the temperature (pressure) inside the condenser 6, such as by reducing the amount of refrigerant generated and lowering the concentration of the absorption liquid, the concentration of the absorption liquid can be stabilized and the temperature of the hot water taken out can be kept constant.
又、逆に、温度レベルが変化した状態の低温熱
源が発生器5及び蒸発器2に供給されるときは、
この低温熱源水温によつて定まる設定値を制御器
19で演算させ(又は外部から与え)、凝縮器内
の液温を新らたな設定値に保てば、低温熱源の温
度レベルが変化しても追随して安定した温度の温
水取り出しができる吸収ヒートポンプの運転が可
能となる。 Conversely, when a low temperature heat source with a changed temperature level is supplied to the generator 5 and the evaporator 2,
If the set value determined by this low temperature heat source water temperature is calculated by the controller 19 (or given from the outside) and the liquid temperature in the condenser is maintained at the new set value, the temperature level of the low temperature heat source will change. This makes it possible to operate an absorption heat pump that can take out hot water at a stable temperature.
次に、吸収ヒートポンプを停止しようとする場
合、制御器19は停止信号を受けると、まず、第
一に制御弁24を全閉とし、冷却水の流通を遮断
し凝縮器内の液温を設定値より高めるように作動
する。このような作動により、凝縮器6への冷却
水の流通がなくなると、該凝縮器6における冷媒
凝縮は停止され、発生器5における吸収液の濃縮
(冷媒の気化分離)もなくなるので、斯る状態で
熱源流体(低温熱源)の供給をとめれば、吸収液
の濃度を稀釈した状態で吸収ヒートポンプの運転
を停止することとなり、比較的濃度が高く、結晶
線に近い状態で運転をしていた此の種のヒートポ
ンプの運転の安全な停止、すなわち、運転停止中
に吸収液が結晶して再始動の幣害を生じるおそれ
のない運転の停止ができるものである。 Next, when trying to stop the absorption heat pump, upon receiving the stop signal, the controller 19 first fully closes the control valve 24, cuts off the flow of cooling water, and sets the liquid temperature in the condenser. It operates to raise the value higher than the value. Due to this operation, when the flow of cooling water to the condenser 6 is stopped, the refrigerant condensation in the condenser 6 is stopped, and the concentration of the absorption liquid (gasification separation of the refrigerant) in the generator 5 is also stopped. If the supply of the heat source fluid (low-temperature heat source) is stopped in this state, the operation of the absorption heat pump will be stopped with the concentration of the absorption fluid diluted, and the absorption fluid will be operated in a state where the concentration is relatively high and close to the crystal line. The operation of this type of heat pump can be stopped safely, that is, the operation can be stopped without the risk of crystallization of the absorption liquid during the stoppage of operation, which will cause problems when restarting the heat pump.
尚、このような運転の制御は、通常の運転から
の停止のみでなく、吸収ヒートポンプの機内の圧
力の上昇、冷却水温度の異常低下、吸収液濃度の
過剰上昇などの異常状態が機内各部のセンサから
もたらされたときにも同様に冷却水制御弁を閉止
し、凝縮器内の液温を設定値より高めた後に吸収
ヒートポンプの運転を停止するように作動するも
のである。 In addition, this type of operation control is not only applicable to stopping normal operation, but also to detect abnormal conditions such as an increase in pressure inside the absorption heat pump, an abnormal drop in cooling water temperature, or an excessive increase in absorption liquid concentration. When the water is supplied from the sensor, the cooling water control valve is similarly closed and the operation of the absorption heat pump is stopped after the temperature of the liquid in the condenser is raised above the set value.
このように、本発明では、吸収液による冷媒吸
収の温度が吸収液から冷媒を発生させる温度より
も高く、かつ、冷媒の蒸発温度が冷媒の凝縮温度
よりも高く設定された吸収ヒートポンプにおい
て、定常運転時には凝縮器内の液温を設定値に保
つよう冷却水温を制御し、かつ、運転停止時には
凝縮器内の液温を高めるように冷却水量を減らす
制御機構を付設し、該吸収ヒートポンプからの取
り出し温水温度を吸収液の結晶のおそれなく一定
温度に保つ一方、安全な運転停止ができる効果を
有するものである。 As described above, in the present invention, in an absorption heat pump in which the temperature at which the absorption liquid absorbs the refrigerant is higher than the temperature at which the refrigerant is generated from the absorption liquid, and the evaporation temperature of the refrigerant is set higher than the condensation temperature of the refrigerant, A control mechanism is installed to control the cooling water temperature to maintain the liquid temperature in the condenser at the set value during operation, and to reduce the amount of cooling water to raise the liquid temperature in the condenser when the operation is stopped. This has the effect of maintaining the temperature of the hot water taken out at a constant temperature without the risk of crystallization of the absorbing liquid, while also allowing safe operation shutdown.
第1図は本発明による吸収ヒートポンプの一実
施例を示す機器の構成図、第2図は作動説明用の
デユーリング線図である。
2……蒸発器、3……吸収器、5……発生器、
6……凝縮器、19……制御器、24……制御
弁。
FIG. 1 is a configuration diagram of a device showing an embodiment of an absorption heat pump according to the present invention, and FIG. 2 is a Duering diagram for explaining the operation. 2...evaporator, 3...absorber, 5...generator,
6... Condenser, 19... Controller, 24... Control valve.
Claims (1)
器とに熱源流体を供給し、吸収器から熱源流体の
温度レベル以上の温度の温水を取り出すよう発生
器、凝縮器、蒸発器、吸収器などを冷媒管及び吸
収液管で気密に配管接続した吸収ヒートポンプに
おいて、該ヒートポンプの定常運転時には凝縮器
内の液温を設定値に保ち、かつ、運転停止時には
凝縮器内の液温を高めるような制御機構が付設さ
れていることを特徴とする吸収ヒートポンプ。1 Supply heat source fluid to the evaporator and generator while circulating cooling water to the condenser, and take out hot water at a temperature higher than the temperature level of the heat source fluid from the absorber. In absorption heat pumps that are airtightly connected with refrigerant pipes and absorption liquid pipes, the temperature of the liquid in the condenser is maintained at the set value during steady operation of the heat pump, and the temperature of the liquid in the condenser is increased when the operation is stopped. An absorption heat pump characterized by being equipped with a control mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14428581A JPS5845469A (en) | 1981-09-11 | 1981-09-11 | Absorption heat pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14428581A JPS5845469A (en) | 1981-09-11 | 1981-09-11 | Absorption heat pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5845469A JPS5845469A (en) | 1983-03-16 |
| JPH0221501B2 true JPH0221501B2 (en) | 1990-05-15 |
Family
ID=15358514
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14428581A Granted JPS5845469A (en) | 1981-09-11 | 1981-09-11 | Absorption heat pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5845469A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5395502B2 (en) * | 2009-04-23 | 2014-01-22 | 株式会社荏原製作所 | Absorption heat pump |
-
1981
- 1981-09-11 JP JP14428581A patent/JPS5845469A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5845469A (en) | 1983-03-16 |
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